Heat transfer enhancement in chemical processes /
Heat Transfer Enhancement in Chemical Processes combines process technologies with heat exchange equipment to study heat transfer enhancement.The book provides guidance for the progress of process technologies and the application of enhanced heat transfer equipment.
| Main Author: | |
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| Corporate Author: | |
| Format: | eBook |
| Language: | English |
| Published: |
Amsterdam :
Elsevier,
2024.
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| Subjects: | |
| Online Access: | Connect to the full text of this electronic book |
Table of Contents:
- Intro
- Heat Transfer Enhancement In Chemical Processes
- Copyright
- Contents
- About the author
- Preface
- Acknowledgments
- Chapter 1: Introduction
- 1.1. Significance of heat transfer enhancement
- 1.1.1. Heat transfer enhancement: An important means of energy conservation and emission reduction
- 1.1.2. Positive effects of heat transfer enhancement on cost saving
- 1.1.3. Important contribution of heat transfer enhancement to energy conservation and emission reduction in chemical industry
- 1.2. Progresses in heat transfer enhancement technology
- 1.2.1. Heat transfer enhancement technology of heat exchanger
- 1.2.2. Optimization technology of heat exchanger network
- 1.2.2.1. Heuristics
- 1.2.2.2. Mathematical programming method
- 1.3. Engineering application of heat transfer enhancement
- 1.3.1. Engineering strategy of innovative heat transfer enhancement
- 1.3.2. Heat transfer enhancement of equipment and components for special technologies, mediums, and processes
- 1.3.3. Heat transfer enhancement of processes
- 1.3.3.1. Crude oil distillation unit-The best application demonstration of pinch point technology
- 1.3.3.2. FCC unit-Heat exchanger network for hot end threshold problem
- 1.3.3.3. Hydrogenation unit-Coordinated heat transfer enhancement of processes and equipment and components
- 1.3.3.4. Ethylene unit-Optimal utilization of cold energy
- 1.3.3.5. Aromatics complex unit-Heat source integration and optimal utilization of low-temperature heat
- 1.4. Heat transfer enhancement of the whole plant
- 1.4.1. Direct heat supply and storage of materials in the whole plant
- 1.4.2. Intensive design of process unit
- 1.4.3. Generation of higher pressure grade steam for cascade optimization and reduction of fuel consumption.
- 1.4.4. Recycle and optimize the utilization of low-temperature heat resources in the whole plant
- 1.4.5. Cascade utilization of cooling water system
- References
- Chapter 2: Basic principles and method of heat transfer enhancement
- 2.1. Basic principles of heat transfer enhancement
- 2.1.1. Basic theory of heat transfer enhancement of heat exchangers
- 2.1.2. Mechanism analysis of convective heat transfer enhancement
- 2.1.3. Evaluation method of heat transfer enhancement performance
- 2.2. Heat transfer enhancement technology
- 2.2.1. Heat transfer enhancement process without phase transition
- 2.2.1.1. Artificial rough surface and irregular surface method
- 2.2.1.2. Extended surface [1,2]
- 2.2.1.3. Vibration method
- 2.2.1.4. Fluid rotation method (inserts)
- 2.2.1.5. Other heat transfer enhancement technologies
- 2.2.2. Heat transfer enhancement of boiling process
- 2.2.2.1. Enhanced nucleation site activity
- 2.2.2.2. Nanofluids
- 2.2.2.3. Surfactant
- 2.2.3. Heat transfer enhancement of condensation process
- 2.2.3.1. Surface condensation heat transfer and enhancement
- 2.2.3.2. Characteristics and enhancement of condensation heat transfer in channel
- 2.2.4. Fouling and cleaning
- 2.3. Commonly used enhanced heat transfer elements and equipment
- 2.3.1. Shell and tube heat exchanger
- 2.3.1.1. Shell side heat transfer enhancement technology
- Enhanced heat transfer tube
- Nonsegmental baffle
- 2.3.1.2. Enhanced heat transfer technology in tube
- 2.3.1.3. Compound heat transfer enhancement technology
- 2.3.1.4. Other heat transfer enhancement technologies
- 2.3.2. Plate heat exchanger
- 2.3.2.1. Corrugated plate heat exchanger
- 2.3.2.2. Spiral plate heat exchanger
- 2.3.2.3. Plate fin heat exchanger
- 2.3.3. Tubular fired heater
- 2.3.3.1. Enhanced heat transfer technology of tube outside.
- 2.3.3.2. Enhanced heat transfer technology in tube
- 2.3.3.3. Enhanced heat transfer technology for waste heat recovery
- 2.3.3.4. Case of heat transfer enhancement of heating
- 2.4. Heat transfer network synthesis technology
- 2.4.1. Basic concept of pinch point technology
- 2.4.1.1. Temperature enthalpy graph
- 2.4.1.2. Composite curve
- 2.4.1.3. Meaning of pinch point
- 2.4.1.4. Determination of pinch point of process system
- 2.4.1.5. Pinch point design method of heat exchanger network
- 2.4.2. Optimal design of threshold problem heat exchanger network
- 2.4.2.1. Analysis of hot end threshold problem heat exchanger network
- 2.4.2.2. Optimization design block diagram for hot end threshold problem heat exchanger network
- 2.4.3. Example analysis of heat exchanger network in FCC unit
- 2.4.3.1. Overview of heat exchanger network in FCC unit
- 2.4.3.2. Improvement of heat exchanger network with the goal of maximum steam generation
- 2.4.3.3. Improvement of heat exchanger network with the goal of maximum heat integration of FCC unit and atmospheric and ...
- References
- Chapter 3: Heat transfer enhancement in typical oil refining units
- 3.1. Crude oil distillation unit
- 3.1.1. Brief description of process
- 3.1.2. Analysis of heat energy characteristics
- 3.1.3. Optimization of process energy consumption and heat exchanger network
- 3.1.3.1. Process energy optimization
- 3.1.3.2. Optimization of heat exchanger network
- 3.1.4. Heat transfer enhancement technology using elements
- 3.1.4.1. Heat exchange system of flash column
- 3.1.4.2. Atmospheric column heat exchange system
- 3.1.4.3. Heat exchange system of vacuum column
- 3.1.4.4. Stabilizer heat exchange system
- 3.1.5. Summary
- 3.2. Catalytic cracking unit
- 3.2.1. Brief description of process
- 3.2.2. Analysis of heat energy characteristics.
- 3.2.3. Process enhancement and integration on heat transfer
- 3.2.3.1. High-temperature-level heat recovery and utilization
- 3.2.3.2. Medium-temperature heat recovery and utilization
- 3.2.3.3. Low-level temperature heat recovery and utilization
- 3.2.4. Heat transfer enhancement technology using elements
- 3.2.4.1. Heat transfer enhancement of the reaction section
- 3.2.4.2. Heat transfer enhancement of the fractionation section
- 3.2.4.3. Heat transfer enhancement of absorption-stabilization section
- 3.2.5. Summary
- 3.3. Hydrocracking unit
- 3.3.1. Brief description of process
- 3.3.2. Analysis of heat energy characteristics
- 3.3.3. Process enhancement and integration on heat transfer
- 3.3.3.1. Optimization of heat transfer process by pinch point analysis technology
- 3.3.3.2. Heat transfer enhancement of the process optimization
- 3.3.4. Heat transfer enhancement technology using elements
- 3.3.4.1. Enhancing of heat transfer component in reaction section
- 3.3.4.2. Enhanced heat transfer component in the fractionation section
- 3.3.5. Summary
- 3.4. Hydrotreating unit
- 3.4.1. Brief description of process
- 3.4.2. Analysis of heat energy characteristics
- 3.4.3. Process enhancement and integration on heat transfer
- 3.4.3.1. Heat transfer enhancement of process optimization
- 3.4.3.2. Enhancing process by making full use of reaction heat
- 3.4.4. Heat transfer enhancement technology using elements
- 3.4.4.1. Application of coil-wound heat exchanger in hydrotreating unit
- 3.4.4.2. Application of shell and plate heat exchanger in hydrotreating unit
- 3.4.4.3. Other applicable enhancement components
- 3.4.5. Summary
- 3.5. Heavy oil hydrotreating unit
- 3.5.1. Brief introduction of process
- 3.5.2. Analysis of heat energy characteristics
- 3.5.2.1. Heat released from reaction.
- 3.5.2.2. Heat provided by the furnace
- 3.5.2.3. Analysis of heat transfer process characteristics
- 3.5.3. Process enhancement and integration on heat transfer
- 3.5.3.1. Selection and optimization of high-pressure heat exchanger network
- 3.5.3.2. Optimization of low-pressure heat exchanger network
- 3.5.3.3. Heat analysis and utilization of fractionator
- 3.5.3.4. Optimization of units heat combination and integration
- 3.5.3.5. Other process optimization for heat transfer enhancement
- 3.5.4. Heat transfer enhancement technology using elements
- 3.5.4.1. Feed heat exchange system
- 3.5.4.2. High-pressure heat exchange system
- 3.5.4.3. Fractionation heat transfer system
- 3.5.5. Summary
- 3.6. Hydrogen production unit
- 3.6.1. Brief introduction of process
- 3.6.2. Analysis of heat energy characteristics
- 3.6.3. Heat optimal utilization of different temperature levels
- 3.6.3.1. Heat utilization of high temperature level
- 3.6.3.2. Utilization of waste heat at medium temperature level
- 3.6.3.3. Low-level temperature potential waste heat utilization
- 3.6.4. Heat transfer enhancement technology using elements
- 3.6.4.1. MT shift gas heat exchange system
- 3.6.4.2. Steam heat exchange system
- 3.6.5. Summary
- 3.7. Delayed coking unit
- 3.7.1. Brief description of process
- 3.7.2. Analysis of heat energy characteristics
- 3.7.3. Process enhancement and integration on heat transfer
- 3.7.3.1. Enhancement technology of feed heat exchange process
- 3.7.3.2. Fractionation section of heat transfer enhancement technology
- 3.7.3.3. The heat integration of absorption and stability section and the coking section to reduce steam consumption
- 3.7.3.4. Application of heat transfer enhancement technology in vent tower
- 3.7.3.5. Low temperature heat utilization
- 3.7.4. Heat transfer enhancement technology using elements.